JPH0380985A - Apparatus for removing pollutant in liquid - Google Patents
Apparatus for removing pollutant in liquidInfo
- Publication number
- JPH0380985A JPH0380985A JP21693489A JP21693489A JPH0380985A JP H0380985 A JPH0380985 A JP H0380985A JP 21693489 A JP21693489 A JP 21693489A JP 21693489 A JP21693489 A JP 21693489A JP H0380985 A JPH0380985 A JP H0380985A
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- water
- bubbles
- foam
- fish
- tank
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Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は養殖漁業、活魚輸送、魚飼育などの分野、およ
び食品工業、例えば米のとぎ汁などにおける廃水の処理
における汚濁物質の除去装置に関するものである。[Detailed Description of the Invention] [Field of Industrial Application] The present invention relates to a device for removing pollutants in the fields of aquaculture and fishing, transport of live fish, fish breeding, etc., and in the food industry, for example, in the treatment of wastewater in rice washing water, etc. It is.
[従来の技術]
現在実用化されている活魚の養殖あるいは輸送システム
では、主として空気や純酸素などを水中へ供給して活魚
の生命維持をはかることを目的とするものであり、魚の
長期間の飼育ができても、老廃物の水中への蓄積などに
より、衛生的な水環境の維持は困難であった。[Prior art] In the live fish farming and transportation systems that are currently in practical use, the main purpose is to supply air, pure oxygen, etc. into the water to maintain the life of the live fish. Even if it were possible to raise them, it was difficult to maintain a sanitary water environment due to the accumulation of waste products in the water.
特に、ビブリオ菌等の有害生菌の除去については、活魚
輸送や魚飼育などにおいて有効な手段はなく、活魚のビ
ブリオ菌等による汚染などは放置せられているのが実情
である。In particular, regarding the removal of harmful living bacteria such as Vibrio bacteria, there is no effective means for transporting or breeding live fish, and the reality is that live fish are left uncontaminated by Vibrio bacteria.
しかし、人の衛生上および魚の生命維持の両面より、有
害菌および汚濁物質を除去する改善は緊急の課題である
。However, improvements to remove harmful bacteria and pollutants are an urgent issue from both human hygiene and fish life support perspectives.
また、食品工業で生ずる大量の廃水、例えば米のとぎ汁
などの処理では、曝気槽と沈澱槽とを用いる大規模な装
置を必要としており、より簡単な装置が望まれている。Furthermore, the treatment of large amounts of wastewater generated in the food industry, such as rice rinse water, requires large-scale equipment using an aeration tank and a sedimentation tank, and a simpler equipment is desired.
泡を用いて水の中の懸濁物質を除去する技術に関連する
ものとして、浮遊選鉱法として泡を利用する多くの例が
知られている。これは空気を散気管を通じ水中に放出し
、泡をつくり、それに汚濁物質または金属分などを耐着
させ浮上分離するものであり、泡を生成する目的で表面
活性剤が用いられている。As related to the technology of using foam to remove suspended solids in water, many examples of the use of foam as flotation methods are known. In this method, air is released into the water through an aeration tube to create bubbles, and pollutants or metals are prevented from adhering to the bubbles and floated and separated.A surfactant is used for the purpose of generating the bubbles.
しかし、浮遊選鉱法による方式で利用されている泡の大
きさは大きく、ビブリオ菌等の有害菌を除去するには不
向きのものであり、今日まで、泡を用いてビブリオ菌等
を除去した例はみられない。However, the size of the bubbles used in the flotation method is large and unsuitable for removing harmful bacteria such as Vibrio bacteria.To date, there have been no examples of using bubbles to remove Vibrio bacteria. I can't see it.
また、魚の生命維持や食品工業などにおいては泡の生成
に表面活性剤を使用することは不適当であることは論を
待たない。Furthermore, it goes without saying that it is inappropriate to use surfactants to generate foam in the life support of fish and in the food industry.
[発明が解決しようとする課題]
従って本発明の課題は、養殖漁業、活魚輸送、魚飼育な
どの分野、および食品工業の廃水における有害菌等の汚
濁物質を、泡を利用し、かつ表面活性剤を用いることな
く連続的に除去する装置を提供せんとするものである。[Problems to be Solved by the Invention] Accordingly, an object of the present invention is to remove pollutants such as harmful bacteria from wastewater in fields such as aquaculture, live fish transportation, and fish breeding, as well as food industry wastewater, by using foam and surface active material. It is an object of the present invention to provide a device for continuous removal without using a chemical agent.
[課題を解決するための手段]
前記課題を解決するために本発明者等は、下記の項目に
ついて検討を重ねた。[Means for Solving the Problems] In order to solve the above problems, the present inventors have repeatedly studied the following items.
〈1〉活魚輸送や食品工業などにおいては水発泡のため
に添加する表面活性剤の添加はできないので、発泡を超
微小気泡とすることが必要であり、そのために適当なエ
アレータ−を採択せねばならない。<1> In the transport of live fish and the food industry, etc., it is not possible to add surfactants for water foaming, so it is necessary to foam into ultra-fine bubbles, and for this purpose it is necessary to select an appropriate aerator. Must be.
本発明の発明者の一人である佐藤鐵三部の発明にかかる
曝気装置(特公昭62−34436号等)は簡単に超微
細気泡による安定した泡を発生させるのに最適であるの
で、この装置を活用する。The aeration device (Japanese Patent Publication No. 62-34436, etc.) invented by Sato Tetsusanbe, one of the inventors of the present invention, is ideal for easily generating stable foam made of ultra-fine bubbles, so this device Make use of it.
(2)活魚輸送における魚の生命維持や魚を生のまま食
する活魚料理等における人の衛生を考える時に水を含む
環境における有害なバクテリア、特にビブリオ菌を泡で
除去できることが必要である。(2) When considering the life support of fish during transport of live fish and human hygiene in live fish dishes where fish are eaten raw, it is necessary to be able to remove harmful bacteria, especially Vibrio bacteria, in environments containing water using foam.
(3)泡を連続的に除去しようとする場合には泡と液体
との界面の位置を常にほぼ一定の位置に保持する必要が
ある。そうしないと泡ばかりでなく中の水の殆ど全部を
益田させて魚をいためたり、また泡が出ない状況が長く
続くと、魚の分泌する成分等が蓄積し悪い影響を及ぼす
。(3) When attempting to remove bubbles continuously, it is necessary to maintain the position of the interface between the bubbles and the liquid at a substantially constant position. If you do not do this, not only the bubbles but also almost all of the water inside will be absorbed, damaging the fish, and if the situation continues for a long time without bubbles, components secreted by the fish will accumulate and have a negative effect.
そこで、これらに対処できる制御を行う必要がある。Therefore, it is necessary to perform control that can deal with these problems.
(4)装置としてコンパクトでかつ能率よく泡分離をは
かれるものでなければならない。(4) The device must be compact and capable of efficient foam separation.
そのためには本発明者らによる曝気装置の特長を生かし
、またその欠点を補うことが必要である。To this end, it is necessary to take advantage of the features of the aeration device developed by the present inventors and to compensate for its shortcomings.
(5)泡による米のとぎ汁などの汚水処理においては流
水の速度を速くしても処理できる処理能力をもつもので
ある必要がある。(5) In the treatment of waste water such as rice washing water using foam, it is necessary to have a treatment capacity that can handle even if the flow rate is increased.
上記諸項目について鋭意検討の結果、本発明を完成した
。As a result of intensive study on the above items, the present invention was completed.
すなわち、本発明は、
1)回転するインペラーの背面に発生する負圧を利用し
て液中に空気を導入し、泡を発生させる自吸引方式の泡
発生装置を具備してなることを特徴とする液中の汚濁物
質除去装置、
2)液面位置の制御手段を有する前記1〉の液中の汚濁
物質除去装置、
3〉液体が回転するインペラーにより、上部から下部方
向に流れる前記1〉の液中の汚濁物質除去装置、
4)泡の回転ベクトルを打消す1以上の隔壁板を設けて
なることを特徴とする前記1〉の液中の汚濁物質除去装
置、
である。That is, the present invention is characterized in that: 1) it is equipped with a self-suction type foam generating device that generates bubbles by introducing air into the liquid using negative pressure generated on the back surface of a rotating impeller; 2) The device for removing contaminants from the liquid according to item 1 above, which has means for controlling the liquid level; 3) The device from item 1 above, in which the liquid flows from the top to the bottom by the rotating impeller. 4) The device for removing contaminants from a liquid according to item 1 above, characterized in that the device is provided with one or more partition plates for canceling the rotational vector of bubbles.
本発明の汚濁物質除去装置は本発明者による曝気装置(
以下、力−ヴアスエアレーターという。〉を泡発生の手
段として採用しているところに一つの大きな特長を持っ
ている。The pollutant removal device of the present invention is an aeration device (
Hereinafter, it will be referred to as force-vous aerator. 〉 is used as a means of generating bubbles, which is one of its major features.
力−ヴアスエアレーターは第2図に1例を示すようにモ
ーター(図示せず)により高速にて回転する軸13は中
空軸であり、その下端に上円板14と下円板15および
翼板16がつき、軸の回転で回転する。As shown in FIG. 2 as an example, the force-vous aerator has a hollow shaft 13 that is rotated at high speed by a motor (not shown), and has an upper disk 14, a lower disk 15, and a hollow shaft at its lower end. A vane plate 16 is attached and rotates by rotation of the shaft.
水中で翼板16が回転するとその背後が負圧を発生する
ことになり軸端の両円板の中の軸に設けた多数の空気孔
17を通して上部の空気を吸い込み超微小気泡18とし
て水中に放出する。When the vane plate 16 rotates underwater, negative pressure is generated behind it, and the air from the upper part is sucked in through the numerous air holes 17 provided on the shaft in both discs at the end of the shaft, and is submerged as ultra-fine bubbles 18. released into the
その特色とするところは、超微小気泡18が発生し、そ
の運動の方向が回転軸に対し直角な水平面内に生ずるこ
とであり、回転軸に直角な平面内に気泡を遠心力で分散
させ水との混和をよくするだけでなく、狭い水槽の中で
良好な泡をつくりうる事である。The feature is that ultra-micro bubbles 18 are generated and the direction of their movement is in a horizontal plane perpendicular to the rotation axis, and the bubbles are dispersed by centrifugal force in the plane perpendicular to the rotation axis. Not only does it mix well with water, but it can also create good bubbles in a small aquarium.
泡は水中に浮かんでいる汚濁物質の浮遊物を陶管する機
能を持っており、その陶管は基本的に泡の表面積に比例
するが、泡は微小な集まりとなればなるほど大きな表面
積を持つので泡を利用する汚濁物質除去装置の性能は超
微小泡を如何にして発生できるかにかかっている。Bubbles have the function of trapping suspended pollutants floating in water, and the tube is basically proportional to the surface area of the bubbles, but the smaller the bubbles are, the larger the surface area becomes. Therefore, the performance of a pollutant removal device that uses bubbles depends on how it can generate ultrafine bubbles.
その点、カーヴ?スエアレーターはこの超微小泡の大量
発生に最適であり、他の如何なる泡発生機構より優れて
いるといえる。On that point, Carve? The spoolator is ideal for generating large amounts of ultra-fine bubbles, and can be said to be superior to any other bubble generation mechanism.
特に、後の実施例から明らかなとおり超微小泡は水中の
どブリオ菌等のバクテリアを泡の中にとり込むと考えら
れ、この泡を分離することによってビブリオ菌等を有効
に除去できることは本発明の最大の特長である。In particular, as will be clear from the later examples, it is thought that ultrafine bubbles take in bacteria such as B. Throat bacterium in the water, and the present invention shows that by separating these bubbles, bacteria such as Vibrio bacterium can be effectively removed. This is its biggest feature.
次に細部機構として泡と水面との境界面と泡の上面を検
出することにより汚濁物質除去装置内の水面を常にある
適当な高さに保ち、それにより泡の益田を最適に保つも
のである。この手段として排出バルブの制御を行なった
。Next, as a detailed mechanism, by detecting the interface between the bubbles and the water surface and the top surface of the bubbles, the water surface inside the pollutant removal device is always maintained at a certain appropriate height, thereby maintaining the optimum level of bubbles. . As a means of achieving this, the discharge valve was controlled.
一方、汚濁物質を除去するための泡は安定して静かに上
昇することが望ましいが、力一ヴ7スエアレーターによ
り与えられる回転のベクトルは安定した泡の発生には有
害である。そこでこの回転ベクトルを打消すため縦の隔
壁板(邪魔板)を設けるなどの改良を加え、小型のタン
クで処理できる水量を極力多くすることにより実用性を
高め、また他の食品工業などにおける米のとぎ汁などの
汚水処理をも可能にした。On the other hand, although it is desirable for the foam to remove pollutants to rise steadily and quietly, the vector of rotation provided by the force aerator is detrimental to stable foam generation. In order to counteract this rotational vector, we have made improvements such as installing vertical bulkheads (baffle plates), and by increasing the amount of water that can be treated with a small tank as much as possible, we have improved its practicality. It also made it possible to treat sewage such as sewage water.
[実施例] 以下、本発明の装置を実施例により説明する。[Example] Hereinafter, the apparatus of the present invention will be explained using examples.
第1図は本発明の実施例として鯛の輸送、および輸送後
48時間のテストを実施した汚濁物質除去装置を備えた
活魚槽の概要を示すものである。FIG. 1 shows an outline of a live fish tank equipped with a pollutant removal device in which sea bream was transported and tested for 48 hours after transport as an example of the present invention.
第1図において魚水槽1は水槽容積9501で中に海水
8901を満し、中に鯛3を50尾(体重約IKy/尾
〉入れている。力一ヴ7スエアレータ−4はモーター5
により回転し空気を水中に放出すると共に泡をつくる。In Fig. 1, the fish tank 1 has a tank volume of 9501, is filled with seawater 8901, and contains 50 sea bream 3 (weighing approximately IKy/fish).
It rotates and releases air into the water, creating bubbles.
モーター5は400Wのものである。The motor 5 is of 400W.
海水2はポンプ6により魚水槽1からくみ出され装置内
を循環する。泡除去用ダクト7は表面に浮かんだ泡を集
めるものであり、泡は泡溜槽8に滞留して液化され、液
化水の貯留槽9にたまりドレーンバルブ10により糸外
に排出される。Seawater 2 is pumped out of the fish tank 1 by a pump 6 and circulated within the apparatus. The foam removal duct 7 collects foam floating on the surface, and the foam is retained in a foam reservoir tank 8 and liquefied, collected in a liquefied water reservoir tank 9, and discharged to the outside of the thread by a drain valve 10.
−5泡除去された海水は濾過装置11を通って、パイプ
12により魚水槽1に返される。なお、濾過装置は活性
炭、ゼオライト、ミネラル石などより構成される。本装
置を使用して活魚(鯛)50尾を50にトラック輸送し
、その後更に合計48時間にわたり試験計測を行なった
。-5 The seawater from which bubbles have been removed passes through a filter 11 and is returned to the fish tank 1 through a pipe 12. The filtration device is made of activated carbon, zeolite, mineral stone, etc. Using this device, 50 live fish (sea bream) were transported by truck to 50, and then test measurements were conducted for a total of 48 hours.
計測は水温、濁度、溶存酸素、溶解性有機物の各項目に
わたって行なわれた。Measurements were taken of water temperature, turbidity, dissolved oxygen, and dissolved organic matter.
この力一ヴ7スエアレータ−4を汚濁物質除去装置の中
で運転した時の経過時間対水質の変化を第3図に示す。FIG. 3 shows the change in water quality versus the elapsed time when this force 7 aerator 4 was operated in a pollutant removal device.
魚槽内の水温はW丁(・)として示すように略一定16
.6〜17,1℃に保たれた。The water temperature in the fish tank is approximately constant as shown by W (・)16
.. The temperature was kept at 6-17.1°C.
魚槽水のpH(ム)は成魚前pH8,19であったが時
間経過に伴って一時的に2回低下し、その後徐々に上昇
してpH7,86まで回復した。pHの低下はNO3窒
素濃度の増加とco2の濃度の増加が原因と考えられる
。魚槽水の溶存酸素濃度(Do)(○〉はほぼ飽和濃度
(7,61m1/J、17℃)を保った。これはカーヴ
7スエアレーターによる鯛の酸素消費を上まわる酸素の
水への供給によるものである。The pH of the fish tank water was 8.19 before the fish became adults, but it temporarily decreased twice over time, and then gradually increased and recovered to pH 7.86. The decrease in pH is thought to be caused by an increase in NO3 nitrogen concentration and an increase in CO2 concentration. The dissolved oxygen concentration (Do) (○) in the fish tank water was maintained at almost the saturated concentration (7.61 m1/J, 17°C).This is due to the supply of oxygen to the water that exceeds the oxygen consumption of the sea bream by the Carve 7 Aerator. This is due to
魚槽水の溶解性有機物(DOC>(II)は実験開始時
には6.2mg/fJであったが、15時間程度までは
0,7■/1・hの割合で直線的に増加し、15時間以
降はその割合が低下し、27時間以後は約0.07mg
/j ・hの低い割合で増加した。一方泡液化水のDO
C11度(図示せず)は最初の6時間では49.5my
/jであったが、39〜45時間では923my/1の
高濃度に達した。Dissolved organic matter (DOC>(II) in fish tank water was 6.2 mg/fJ at the beginning of the experiment, but it increased linearly at a rate of 0.7 μ/1 h until about 15 hours, and After 27 hours, the percentage decreases, and after 27 hours, it is about 0.07 mg.
/j ・h increased at a low rate. On the other hand, DO of foam liquefied water
C11 degrees (not shown) is 49.5 my in the first 6 hours.
/j, but reached a high concentration of 923 my/1 in 39 to 45 hours.
DOCは泡液化水に高濃度に濃縮されるが、常に泡の溢
出を適切かつ大量に行うことの重要性が理解された。Although DOC is highly concentrated in foam liquefied water, it has been realized that it is important to always perform adequate and large amount of foam spillover.
一方魚槽水の濁度(Turbidity ) (Δ)
は実験の全期間を通じ増大することなく一定に保たれ、
水の清浄化効果が泡除去により得られることを示してい
る。On the other hand, turbidity (Δ) of fish tank water
remains constant without increasing during the entire period of the experiment,
This shows that the water purification effect can be obtained by removing bubbles.
これをより詳細に説明するのが第4図であり、泡液化水
の濁度値の測定から、もし泥分が泡により除去せられず
増加をつづけたら点線(・)に示すように濁度は45時
間後には11度になる。泡による除去で実線(○)に示
すように2度以下に保たれ、泡除去による大きな効果を
示している。This is explained in more detail in Figure 4. From the measurement of the turbidity value of foam liquefied water, if the mud continues to increase without being removed by foam, the turbidity will increase as shown by the dotted line (・). will be 11 degrees in 45 hours. As shown by the solid line (○), the temperature was kept at 2 degrees or less due to bubble removal, indicating the great effect of bubble removal.
−六本実験で発見せられた最大の成果は第5図に示すよ
うなバクテリア菌、特に病原ビブリオ菌の泡除去による
減少である。- The greatest result discovered in the Rokumoto experiment was the reduction of bacteria, especially pathogenic Vibrio bacteria, by removing the foam, as shown in Figure 5.
魚槽水の一般生菌(○〉は成魚前には3.1×103
(CFU/d)であったものが成魚直後には約2倍に増
加し、その後27時間後には5.4×105まで増加し
たものの48時間後でもそれ以上の増加は見られず、一
方泡液化水の一般生菌(・〉は成魚直後で8.7XIQ
5であったものが27時間後には5.9 X107.4
8時間後には7.0X1Q と約108オーダーまで
増加し、泡による除去効果があることがわかった。General viable bacteria in fish tank water (○) is 3.1 x 103 before the fish mature.
(CFU/d) increased approximately twice as soon as the fish matured, and then increased to 5.4 x 105 after 27 hours, but no further increase was observed even after 48 hours. General viable bacteria in liquefied water (・〉 is 8.7XIQ immediately after adulthood)
What was 5 became 5.9 x 107.4 after 27 hours.
After 8 hours, the amount increased to 7.0×1Q, about 108 orders of magnitude, indicating that the bubbles had a removal effect.
一方、生の魚を食する時に中毒事故の原因となるビブリ
オ菌は第5図中Δに示すように、実験開始から終了まで
を通じて魚槽水からは極めて低い値しか検出されず、一
方泡液化水(図中のム参照)からは27時間後に4.2
XIO3(CFU/岨、48時間後には3.9X10
’ (CFU/rr11>と高濃度の病原ビブリオが
検出された。On the other hand, as shown by Δ in Figure 5, Vibrio bacteria, which causes poisoning accidents when eating raw fish, was only detected at extremely low levels in the fish tank water from the start to the end of the experiment; 4.2 after 27 hours from water (see mu in the figure)
XIO3 (CFU/岨, 3.9X10 after 48 hours
'A high concentration of pathogenic Vibrio (CFU/rr11>) was detected.
以上のテスト結果を分析すると、ビブリオ菌の方がより
効率よく泡に濃縮されることが明らかであり、その原因
は菌の大きざがビブリオ菌の方が大きいことも原因の一
つであろう。Analyzing the above test results, it is clear that Vibrio bacteria are more efficiently concentrated into foam, and one of the reasons for this may be that Vibrio bacteria are larger in size. .
なお泡の発生量(速度)は液化した水量で表わすと平均
210〜225af/hであった。泡から液化された合
計水量は最初の魚水槽の水量(890M>に対して48
時間で約1.2%と少なく、これを増大させることによ
り泡分離による水質の改善はより大きくなると推定され
る。Note that the amount of foam generation (speed), expressed as the amount of liquefied water, was on average 210 to 225 af/h. The total amount of water liquefied from the foam was 48% for the initial fish tank water volume (890M>).
It is estimated that the improvement in water quality due to foam separation will be greater by increasing this amount, which is about 1.2% per hour.
一方、魚を水槽に入れた直後、輸送車が走り出した直後
などに魚に緊張が加わるので魚による分泌物が多く出て
大量の泡が発生し、泡の益田口から泡が溢れ出るのが目
視せられ、その他の時には泡液化水が出ないことなどが
観察され、従って泡の益田速度は状況に応じて制御する
ことが好ましい。On the other hand, immediately after putting the fish in the aquarium or immediately after the transportation vehicle starts running, the fish become stressed, so a lot of secretions are produced by the fish, and a large amount of bubbles are generated, and the bubbles overflow from the Masuda mouth of the bubbles. At other times, it is observed that foam liquefied water does not come out, so it is preferable that the Masuda speed of foam is controlled depending on the situation.
第6図に示すのは本発明を例示した改良されたカーヴア
スエアレーター付ビブリオ菌等汚濁物質除去装置の作動
説明図である。FIG. 6 is an explanatory diagram of the operation of an improved device for removing contaminants such as Vibrio bacteria with a curved aerator, which exemplifies the present invention.
水タンク19の中には水槽水(魚を含む)または米のと
ぎ汁のような液体が入っている。The water tank 19 contains liquid such as aquarium water (including fish) or rice water.
この水タンク19の水は吸水ポンプ20により泡除去タ
ンク21に管22を通して力−ヴアスエアレータ−23
より上部に送水される。The water in this water tank 19 is passed through a pipe 22 to a foam removal tank 21 by a water suction pump 20 and then to a foam aerator 23.
Water is sent to the upper part.
力−ヴアスエアレータ−23はモーター24により中空
軸25を介して水中で高速回転され超微小気泡26を降
下する水の流れに対し直角の平面内(水平面)に放射状
に放出し、水との混和をよくし、水の中に含まれたビブ
リオ菌等のバクテリアおよび汚濁物質を泡に吸着して浮
上させる。The force-vous aerator 23 is rotated at high speed in water via a hollow shaft 25 by a motor 24, and emits ultra-micro bubbles 26 radially in a plane (horizontal plane) perpendicular to the descending water flow, so that they mix with the water. The foam absorbs bacteria such as Vibrio bacteria and pollutants contained in the water and floats them to the surface.
この浮上する泡は出来るだけ静かに浮び上っていくこと
が、泡による吸着性を向上させるのに大事である。It is important for the floating bubbles to float as quietly as possible in order to improve the suction properties of the bubbles.
その際力一ヴ7スエアレータ−23により発生された超
微小気泡26が持っている回転の速度ベクトルは泡の安
定上昇には有害である。At this time, the rotational velocity vector of the ultra-fine bubbles 26 generated by the force aerator 23 is detrimental to the stable rise of the bubbles.
そこで、タンクの内側に隔壁板(邪魔板)27がおかれ
水の回転を打消すよう構成されている。Therefore, a partition plate (baffle plate) 27 is placed inside the tank to counteract the rotation of the water.
この作用により泡は静かに上昇し、液面に集った泡と液
面との境界は時にはエマルジョンの状態となる。これが
原因となって泡だけでなく水まで泡溢出口28より溢出
し、受はタンク29にどっと水が入ってくることがある
。This action causes the bubbles to rise quietly, and the boundary between the bubbles that collect on the liquid surface and the liquid surface sometimes becomes an emulsion. As a result, not only foam but also water may overflow from the foam overflow port 28, and a large amount of water may enter the tank 29 of the receiver.
これをさけるには注意深く液面30を泡溢出口28に対
し、ある適切なレベルに保つことが要求される。To avoid this, it is necessary to carefully maintain the liquid level 30 at an appropriate level relative to the foam overflow port 28.
そのために液面30に浮かんだ小浮体31により液面を
検出しそれにより上下するバー32上部についたセンサ
ー33によりタンク21の出口34のバルブ35を制御
し液面をコントロールする。For this purpose, the liquid level is detected by a small floating body 31 floating on the liquid level 30, and the sensor 33 attached to the upper part of the bar 32, which moves up and down, controls the valve 35 at the outlet 34 of the tank 21 to control the liquid level.
以上のように、液面を最適な高さに保つことを可能にし
、また水面の高さを保つのに出口34のバルブ35を自
動制御する制御回路を組み込むことも本発明の大きな特
長である。As mentioned above, a major feature of the present invention is that it makes it possible to maintain the liquid level at an optimal height, and also incorporates a control circuit that automatically controls the valve 35 of the outlet 34 to maintain the water level. .
一方、本装置による他のテストで、水の送水速度を高く
すればするほど、良好な泡が発生し、送水速度は泡除去
タンク21の水量を1分間で全部循環するくらいの速度
またはこれの2〜3倍の速度としてもよいことが確認さ
れており、本発明の装置は活魚輸送だけでなく食品工業
の米のとぎ汁のような汚濁物を含んだ水の処理にも有効
と考えられる。On the other hand, other tests using this device have shown that the higher the water feeding speed, the better the foam is generated, and the water feeding speed is at a speed that is sufficient to circulate the entire amount of water in the foam removal tank 21 in one minute. It has been confirmed that the speed can be increased by 2 to 3 times, and the device of the present invention is considered to be effective not only for transporting live fish but also for treating water containing pollutants such as rice washing water in the food industry.
第1図は本発明の汚濁物質除去装置を備えた活魚槽例の
概要図、
第2図は本発明の装置で使用する曝気装置例の斜視図、
第3図は本発明装置による活魚水槽水の水温(WT>、
溶解性有機炭素(DOC>、溶存酸素濃度(Do) 、
濁度(Turbidity ) 、および0日の経時変
化を示すグラフ、
第4図は同じく水槽水の濁度および泡液化水の濁度から
推定される本発明装置を使用しない場合の水槽水の濁度
の経時変化を示すグラフ、第5図は同じく本発明の装置
による活魚水槽水の一般生菌数、ビブリオ菌数および泡
液化水中の一般生菌数、ビブリオ菌数の経時変化を示す
グラフ、
第6図は本発明による他の汚濁物質除去装置例の概要図
である。
図中符号:
1・・・無水槽: 2・・・海水; 3・・・鯛; 4
・・・曝気装置; 5・・・モーター: 6・・・ポン
プ; 7・・・泡除去用ダクト; 8・・・泡溜槽:
9・・・泡液化水貯留槽: 10・・・ドレーンバルブ
: 11・・・濾過装置: 12・・・パイプ: 13
・・・回転軸:14・・・上円板: 15・・・下円板
; 16・・・翼板;17・・・孔: 18・・・超微
小気泡; 19・・・水槽;20・・・吸引ポンプ:
21・・・泡除去タンク;22・・・パイプ; 23・
・・曝気装置; 24・・・モーター; 25・・・中
空軸: 26・・・超微小気泡;27・・・隔壁板;
28・・・泡溢出口; 29・・・タンク; 30・・
・液面: 31・・・小浮体: 32・・・バー; 3
3・・・センサー: 34・・・出口:35・・・バル
ブ。Fig. 1 is a schematic diagram of an example of a live fish tank equipped with the pollutant removal device of the present invention, Fig. 2 is a perspective view of an example of an aeration device used in the device of the present invention, and Fig. 3 is a live fish tank water using the device of the present invention. water temperature (WT>,
Soluble organic carbon (DOC>, dissolved oxygen concentration (Do),
A graph showing turbidity and changes over time on day 0. Figure 4 shows the turbidity of aquarium water when the device of the present invention is not used, also estimated from the turbidity of aquarium water and the turbidity of foam-liquefied water. FIG. 5 is a graph showing changes over time in the number of general viable bacteria and Vibrio bacteria in live fish tank water and the number of general viable bacteria and Vibrio bacteria in liquefied foam water using the apparatus of the present invention. FIG. 6 is a schematic diagram of another example of the pollutant removal device according to the present invention. Symbols in the figure: 1... Anhydrous tank: 2... Seawater; 3... Sea bream; 4
... Aeration device; 5... Motor: 6... Pump; 7... Foam removal duct; 8... Foam reservoir tank:
9... Foam liquefied water storage tank: 10... Drain valve: 11... Filtration device: 12... Pipe: 13
... Rotation axis: 14 ... Upper disk: 15 ... Lower disk; 16 ... Wing plate; 17 ... Hole: 18 ... Ultra-micro bubble; 19 ... Water tank; 20...Suction pump:
21... Foam removal tank; 22... Pipe; 23.
...Aeration device; 24...Motor; 25...Hollow shaft: 26...Ultra-fine bubbles; 27...Partition plate;
28... Foam overflow outlet; 29... Tank; 30...
・Liquid level: 31...Small floating body: 32...Bar; 3
3...Sensor: 34...Outlet: 35...Valve.
Claims (1)
て液中に空気を導入し、泡を発生させる自吸引方式の泡
発生装置を具備してなることを特徴とする液中の汚濁物
質除去装置。 2)液面位置の制御手段を有する請求項1記載の液中の
汚濁物質除去装置。 3)液体が回転するインペラーにより、上部から下部方
向に流れる請求項1記載の液中の汚濁物質除去装置。 4)泡の回転ベクトルを打消す1以上の隔壁板を設けて
なることを特徴とする請求項1記載の液中の汚濁物質除
去装置。[Claims] 1) It is characterized by being equipped with a self-suction type foam generating device that generates bubbles by introducing air into the liquid using negative pressure generated on the back surface of a rotating impeller. A device for removing pollutants from liquids. 2) The device for removing contaminants from a liquid according to claim 1, further comprising means for controlling a liquid level position. 3) The device for removing contaminants in a liquid according to claim 1, wherein the liquid flows from the top to the bottom by a rotating impeller. 4) The device for removing contaminants from a liquid according to claim 1, further comprising one or more partition plates for canceling the rotational vector of the bubbles.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1216934A JPH0688017B2 (en) | 1989-08-23 | 1989-08-23 | Device for removing contaminants in liquid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1216934A JPH0688017B2 (en) | 1989-08-23 | 1989-08-23 | Device for removing contaminants in liquid |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0380985A true JPH0380985A (en) | 1991-04-05 |
| JPH0688017B2 JPH0688017B2 (en) | 1994-11-09 |
Family
ID=16696219
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1216934A Expired - Lifetime JPH0688017B2 (en) | 1989-08-23 | 1989-08-23 | Device for removing contaminants in liquid |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0688017B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9912208B2 (en) | 2014-09-26 | 2018-03-06 | Denso Corporation | Drive apparatus |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS52143554A (en) * | 1976-05-26 | 1977-11-30 | United States Filter Corp | System for separating impurties suspended by mixing gas in liquid |
| JPS6447330A (en) * | 1987-08-17 | 1989-02-21 | Kuroki Shigemitsu | Container system for transportation of live fish |
-
1989
- 1989-08-23 JP JP1216934A patent/JPH0688017B2/en not_active Expired - Lifetime
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS52143554A (en) * | 1976-05-26 | 1977-11-30 | United States Filter Corp | System for separating impurties suspended by mixing gas in liquid |
| JPS6447330A (en) * | 1987-08-17 | 1989-02-21 | Kuroki Shigemitsu | Container system for transportation of live fish |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9912208B2 (en) | 2014-09-26 | 2018-03-06 | Denso Corporation | Drive apparatus |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0688017B2 (en) | 1994-11-09 |
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